Hi,
As a scope of project , we are adding new two pipeline pumps in parallel to the existing two pipeline pumps(30 Year old) with similar capacity.
Major difference is that new selected pumps are provided with Variable Frequency Drive (VFD) to meet different flow scenarios economically.
Existing piping system is designed for 68 barg.
Selected new pumps have shut off head of 76.76 barg at 105% rated pump speed.Hence to safeguard existing pipeline from new shut off we are providing,
1. Pressure High High Trip at 67 barg at new pipeline pumps common discharge to stop new pumps.
2. Pressure safety valve at new pipeline pump common discharge line which is set at 68 barg.
I have sized pressure relief valve considering pump blocked in condition as governing case with pump rated flow at rated rpm(liquid relief rate).
But client process engineer comp up with comment that relief rate shall be taken from selected pump curve at 105% rated speed corresponding to set pressure of PSV(68 barg). Which call for higher relief rate.
It will be great help for me, which is right relief rate for PSV sizing with relevant reference guidelines.
I am herewith attaching selected pump curve.

FB






